UA42689C2 - method of modernization of reactor for heterogeneous exothermic synthesis and method of heterogeneous exothermic synthesis - Google Patents

method of modernization of reactor for heterogeneous exothermic synthesis and method of heterogeneous exothermic synthesis

Info

Publication number
UA42689C2
UA42689C2 UA94105974A UA94105974A UA42689C2 UA 42689 C2 UA42689 C2 UA 42689C2 UA 94105974 A UA94105974 A UA 94105974A UA 94105974 A UA94105974 A UA 94105974A UA 42689 C2 UA42689 C2 UA 42689C2
Authority
UA
Ukraine
Prior art keywords
boiler
reactor
housing
exothermic synthesis
heterogeneous exothermic
Prior art date
Application number
UA94105974A
Other languages
Russian (ru)
Ukrainian (uk)
Inventor
Умберто Зарді
Умберто Зарди
Джорджо Пагані
Філіппі Ерманно
Original Assignee
Аммоніа Казале С.А.
Аммониа Казале С.А.
Умберто Зарді
Умберто Зарди
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Аммоніа Казале С.А., Аммониа Казале С.А., Умберто Зарді, Умберто Зарди filed Critical Аммоніа Казале С.А.
Publication of UA42689C2 publication Critical patent/UA42689C2/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0417Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor
    • C01C1/0423Cold wall reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0403Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal
    • B01J8/0407Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds
    • B01J8/0415Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds the beds being superimposed one above the other
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496Heating or cooling the reactor
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0447Apparatus other than synthesis reactors
    • C01C1/0452Heat exchangers
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/152Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/0053Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002Chemical plants
    • B01J2219/00018Construction aspects
    • B01J2219/00024Revamping, retrofitting or modernisation of existing plants
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The method of modernization of reactor for heterogeneous exothermic synthesis includes the installation out of the housing of boiler for generation of high pressure steam, connection of boiler with the housing near exhaust nozzle of housing, connection, at least, of one catalytic layer with the inlet collector of gas in the boiler by means of the conduit located in the exhaust nozzle housing with formation of annular air gap. Conduit and air gap form appropriate channels for reacted gases in the direction toward mentioned boiler and from the boiler beyond the limits of the reactor.
UA94105974A 1993-10-29 1994-10-28 method of modernization of reactor for heterogeneous exothermic synthesis and method of heterogeneous exothermic synthesis UA42689C2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH325793 1993-10-29

Publications (1)

Publication Number Publication Date
UA42689C2 true UA42689C2 (en) 2001-11-15

Family

ID=4252066

Family Applications (1)

Application Number Title Priority Date Filing Date
UA94105974A UA42689C2 (en) 1993-10-29 1994-10-28 method of modernization of reactor for heterogeneous exothermic synthesis and method of heterogeneous exothermic synthesis

Country Status (9)

Country Link
US (1) US5882606A (en)
EP (1) EP0650760B1 (en)
CN (1) CN1050532C (en)
AT (1) ATE198426T1 (en)
CA (1) CA2118047C (en)
DE (1) DE69426517D1 (en)
PL (1) PL305653A1 (en)
RU (1) RU2137538C1 (en)
UA (1) UA42689C2 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69829549T2 (en) 1998-01-16 2006-03-23 Ammonia Casale S.A. Process for the in-situ modernization of a heterogeneous synthesis reactor
US6132687A (en) * 1998-05-21 2000-10-17 Kellogg Brown & Root, Inc. Horizontal ammonia converter adapted for high activity catalyst
GB9922940D0 (en) * 1999-09-29 1999-12-01 Ici Plc Catalytic reactor
WO2008009876A2 (en) * 2006-07-19 2008-01-24 Ineos Europe Limited Apparatus and process for the production of olefins
US7867465B2 (en) * 2008-05-29 2011-01-11 Kellogg Brown & Root Llc Cold wall horizontal ammonia converter
CN102261638A (en) * 2011-05-20 2011-11-30 湖南安淳高新技术有限公司 Three-in-one device composed of reactor, waste heat boiler and steam superheater
CN102836673A (en) * 2011-06-24 2012-12-26 阿梅尼亚卡萨莱股份有限公司 Heterogeneous heat emission synthesis reactor
CN103657532B (en) * 2013-12-13 2015-08-26 衢州昀睿工业设计有限公司 Self-loopa chemical synthesis device
EP3658269A4 (en) * 2017-07-27 2021-03-10 Kellogg Brown & Root LLC Method for revamping vertical converters having a flanged pressure shell extension for housing an internal heat exchanger

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4554135A (en) * 1982-11-26 1985-11-19 C F Braun & Co. Ammonia converter
IN165082B (en) * 1985-05-15 1989-08-12 Ammonia Casale Sa
EP0269854B1 (en) * 1986-11-03 1992-12-23 Ammonia Casale S.A. Process for reducing energy consumption in multi-unit reactors for heterogeneoussynthesis and related reactors
US4744966A (en) * 1986-11-20 1988-05-17 Santa Fe Braun Inc. Process for synthesizing ammonia
DE8634276U1 (en) * 1986-12-22 1991-11-14 Uhde Gmbh, 4600 Dortmund, De
EP0355303B2 (en) * 1988-06-27 1995-12-20 Ammonia Casale S.A. Reactor for exothermic heterogeneous synthesis with several catalytic beds and with the external recovery of reaction heat
CH678286A5 (en) * 1989-03-09 1991-08-30 Ammonia Casale Sa
US4907643A (en) * 1989-03-22 1990-03-13 C F Braun Inc. Combined heat exchanger system such as for ammonia synthesis reactor effluent
US5236671A (en) * 1990-09-24 1993-08-17 C. F. Braun, Inc. Apparatus for ammonia synthesis
US5152997A (en) * 1990-12-11 1992-10-06 Theratech, Inc. Method and device for transdermally administering testosterone across nonscrotal skin at therapeutically effective levels

Also Published As

Publication number Publication date
CN1050532C (en) 2000-03-22
RU94039279A (en) 1996-08-20
EP0650760A1 (en) 1995-05-03
ATE198426T1 (en) 2001-01-15
RU2137538C1 (en) 1999-09-20
CN1110626A (en) 1995-10-25
PL305653A1 (en) 1995-05-02
DE69426517D1 (en) 2001-02-08
CA2118047A1 (en) 1995-04-30
CA2118047C (en) 2004-09-07
US5882606A (en) 1999-03-16
EP0650760B1 (en) 2001-01-03

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